MODELING AND SIMULATION OF THE REVERSED FLOW OPERATION OF A FIXED-BED REACTOR FOR METHANOL SYNTHESIS

被引:65
作者
VANDENBUSSCHE, KM [1 ]
NEOPHYTIDES, SN [1 ]
ZOLOTARSKII, IA [1 ]
FROMENT, GF [1 ]
机构
[1] STATE UNIV GHENT,PETROCHEM TECH LAB,KRIJGSLAAN 281,B-9000 GHENT,BELGIUM
关键词
D O I
10.1016/0009-2509(93)80150-O
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The proposed simulation of the reversed flow operation of a fixed-bed reactor for methanol synthesis is based upon a heterogeneous one-dimensional model. Different levels of transient modelling are compared. By using the most sophisticated model, the influence of a number of operating parameters is assessed. Considerable insight into the reactor behaviour is obtained.
引用
收藏
页码:3335 / 3345
页数:11
相关论文
共 32 条
[21]  
SAPUNDZHIEV K, 1988, TEOR OSNOVY KHIM TEK, V22, P349
[22]   PERIODICAL OPERATION OF CHEMICAL PROCESSES AND EVALUATION OF CONVERSION IMPROVEMENTS [J].
SCHADLICH, K ;
HOFFMANN, U ;
HOFMANN, H .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (09) :1375-1384
[23]  
SILVESTON PL, 1987, REACTORS REACTION EN
[24]  
THULLIE J, 1990, UNSTEADY STATE PROCE, P687
[25]  
VANDENBUSSCHE KM, 1992, P EC C ENERGY EFFICI
[26]  
VANDENBUSSCHE KM, IN PRESS
[27]  
VANDENBUSSCHE KM, 1992, 8TH P INT C LARG CHE
[28]  
Villadsen J., 1978, SOLUTION DIFFERENTIA
[29]   MULTIFUNCTIONAL REACTORS [J].
WESTERTERP, KR .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (9-11) :2195-2206
[30]   REACTOR PERFORMANCE WITH PERIODIC-FLOW REVERSAL FOR A MULTISTEP COMPLEX-REACTION [J].
ZAGORUIKO, AN ;
MATROS, YS ;
KUMAR, VR ;
KULKARNI, BD .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (17-18) :4315-4321